PL89663B1 - - Google Patents
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- Publication number
- PL89663B1 PL89663B1 PL1972156002A PL15600272A PL89663B1 PL 89663 B1 PL89663 B1 PL 89663B1 PL 1972156002 A PL1972156002 A PL 1972156002A PL 15600272 A PL15600272 A PL 15600272A PL 89663 B1 PL89663 B1 PL 89663B1
- Authority
- PL
- Poland
- Prior art keywords
- catalyst
- oil
- riser
- zone
- distance
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 claims description 130
- 238000000034 method Methods 0.000 claims description 54
- 229930195733 hydrocarbon Natural products 0.000 claims description 33
- 150000002430 hydrocarbons Chemical class 0.000 claims description 33
- 230000008569 process Effects 0.000 claims description 30
- 238000004231 fluid catalytic cracking Methods 0.000 claims description 8
- 230000008929 regeneration Effects 0.000 claims description 7
- 238000011069 regeneration method Methods 0.000 claims description 7
- 239000003921 oil Substances 0.000 description 45
- 238000006243 chemical reaction Methods 0.000 description 33
- 239000003502 gasoline Substances 0.000 description 20
- 239000002994 raw material Substances 0.000 description 17
- 238000012360 testing method Methods 0.000 description 13
- 239000000047 product Substances 0.000 description 11
- 239000004215 Carbon black (E152) Substances 0.000 description 10
- 239000007788 liquid Substances 0.000 description 10
- 239000007789 gas Substances 0.000 description 9
- 239000000571 coke Substances 0.000 description 8
- 239000010724 circulating oil Substances 0.000 description 6
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 6
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 6
- 238000010517 secondary reaction Methods 0.000 description 6
- 238000000926 separation method Methods 0.000 description 6
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 5
- 150000001336 alkenes Chemical class 0.000 description 4
- 230000001174 ascending effect Effects 0.000 description 4
- 238000009835 boiling Methods 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- 229910021536 Zeolite Inorganic materials 0.000 description 3
- 238000003795 desorption Methods 0.000 description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 239000001282 iso-butane Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000010457 zeolite Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000004523 catalytic cracking Methods 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 235000003197 Byrsonima crassifolia Nutrition 0.000 description 1
- 240000001546 Byrsonima crassifolia Species 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000009420 retrofitting Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000001960 triggered effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US21225271A | 1971-12-27 | 1971-12-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PL89663B1 true PL89663B1 (enrdf_load_stackoverflow) | 1976-12-31 |
Family
ID=22790232
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PL1972156002A PL89663B1 (enrdf_load_stackoverflow) | 1971-12-27 | 1972-06-13 |
Country Status (11)
Families Citing this family (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4064038A (en) * | 1973-05-21 | 1977-12-20 | Universal Oil Products Company | Fluid catalytic cracking process for conversion of residual oils |
| US3990992A (en) * | 1974-04-12 | 1976-11-09 | Standard Oil Company | Regeneration of cracking catalyst in a vessel with a partition forming an upper and lower zone |
| CA1110568A (en) * | 1976-09-30 | 1981-10-13 | James H. Haddad | Fluid cracking process and the method for separating a suspension discharged from a riser cracking zone |
| US4086064A (en) * | 1976-12-06 | 1978-04-25 | Texaco Inc. | Apparatus for fluidized catalytic cracking |
| US4332673A (en) * | 1979-11-14 | 1982-06-01 | Ashland Oil, Inc. | High metal carbo-metallic oil conversion |
| US4482451A (en) * | 1982-09-16 | 1984-11-13 | Uop Inc. | Process for the separation of particulate solids from vapors using a discharge having a helical twist |
| US4397738A (en) * | 1982-09-16 | 1983-08-09 | Uop Inc. | Process for the separation of particulate solids from vapors |
| US4591427A (en) * | 1982-11-24 | 1986-05-27 | Chevron Research Company | Method for vapor recovery for fluidized catalytic cracking processes |
| US4478708A (en) * | 1983-10-11 | 1984-10-23 | Farnsworth Carl D | Method and apparatus for separating fluidized solid particles suspended in gasiform material |
| US4666586A (en) * | 1983-10-11 | 1987-05-19 | Farnsworth Carl D | Method and arrangement of apparatus for cracking high boiling hydrocarbon and regeneration of solids used |
| US4737346A (en) * | 1984-05-21 | 1988-04-12 | Mobil Oil Corporation | Closed cyclone FCC catalyst separation with stripping gas injection and direct steam injection |
| US4741883A (en) * | 1984-07-18 | 1988-05-03 | Mobil Oil Corp. | FCC catalyst separation apparatus |
| US4629552A (en) * | 1984-07-18 | 1986-12-16 | Mobil Oil Corporation | FCC catalyst separation method |
| US4927527A (en) * | 1984-07-18 | 1990-05-22 | Mobil Oil Corporation | Method for reducing overcracking during FCC catalyst separation |
| US4584090A (en) * | 1984-09-07 | 1986-04-22 | Farnsworth Carl D | Method and apparatus for catalytically converting fractions of crude oil boiling above gasoline |
| US4786400A (en) * | 1984-09-10 | 1988-11-22 | Farnsworth Carl D | Method and apparatus for catalytically converting fractions of crude oil boiling above gasoline |
| US4871514A (en) * | 1987-11-09 | 1989-10-03 | Mobil Oil Corporation | Flapper valve |
| US7090081B2 (en) * | 2003-09-05 | 2006-08-15 | Exxonmobil Chemical Patents Inc. | Selectively removing undesirably sized catalyst particles from a reaction system |
| US8691081B2 (en) * | 2009-09-09 | 2014-04-08 | Uop Llc | Process for contacting hydrocarbon feed and catalyst |
| WO2011031378A2 (en) * | 2009-09-09 | 2011-03-17 | Uop Llc | Apparatus and process for contacting hydrocarbon feed and catalyst |
| US20110058989A1 (en) * | 2009-09-09 | 2011-03-10 | Uop Llc | Apparatus for contacting hydrocarbon feed and catalyst |
| US11376558B2 (en) * | 2020-01-13 | 2022-07-05 | Kellogg Brown & Root Llc | Slurry phase reactor with internal cyclones |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2944963A (en) * | 1958-03-03 | 1960-07-12 | Shell Oil Co | Conversion of heavy oils to gasoline using the fluidized catalyst technique |
| US3188184A (en) * | 1960-04-15 | 1965-06-08 | Pullman Inc | Fluid catalytic cracking unit |
| US3092468A (en) * | 1961-05-09 | 1963-06-04 | Kellogg M W Co | Apparatus for handling powdered material |
| US3188185A (en) * | 1961-05-12 | 1965-06-08 | Pullman Inc | Means for converting hydrocarbons |
| US3355380A (en) * | 1965-07-27 | 1967-11-28 | Exxon Research Engineering Co | Controlling catalyst holdup in conversion of hydrocarbons |
| US3607127A (en) * | 1968-04-05 | 1971-09-21 | Pullman Inc | Apparatus for conversion of hydrocarbons |
| US3617496A (en) * | 1969-06-25 | 1971-11-02 | Gulf Research Development Co | Fluid catalytic cracking process with a segregated feed charged to separate reactors |
| US3619415A (en) * | 1969-07-29 | 1971-11-09 | Texaco Inc | Method and apparatus for fluid catalytic cracking |
| US3607129A (en) * | 1970-04-13 | 1971-09-21 | Universal Oil Prod Co | Apparatus for catalytic cracking |
-
1971
- 1971-12-27 US US00212252A patent/US3785962A/en not_active Expired - Lifetime
-
1972
- 1972-06-13 PL PL1972156002A patent/PL89663B1/pl unknown
- 1972-12-13 ZA ZA728826A patent/ZA728826B/xx unknown
- 1972-12-20 GB GB5872372A patent/GB1413978A/en not_active Expired
- 1972-12-22 IT IT55010/72A patent/IT974303B/it active
- 1972-12-22 DE DE2263098A patent/DE2263098C3/de not_active Expired
- 1972-12-22 AU AU50427/72A patent/AU458574B2/en not_active Expired
- 1972-12-27 FR FR7246317A patent/FR2166049B1/fr not_active Expired
- 1972-12-27 BR BR9155/72A patent/BR7209155D0/pt unknown
- 1972-12-27 JP JP734402A patent/JPS5129165B2/ja not_active Expired
- 1972-12-27 CA CA159,910A patent/CA982511A/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| DE2263098A1 (de) | 1973-07-12 |
| IT974303B (it) | 1974-06-20 |
| FR2166049B1 (enrdf_load_stackoverflow) | 1975-11-07 |
| GB1413978A (en) | 1975-11-12 |
| DE2263098B2 (de) | 1974-11-21 |
| CA982511A (en) | 1976-01-27 |
| ZA728826B (en) | 1973-09-26 |
| JPS4876908A (enrdf_load_stackoverflow) | 1973-10-16 |
| FR2166049A1 (enrdf_load_stackoverflow) | 1973-08-10 |
| US3785962A (en) | 1974-01-15 |
| DE2263098C3 (de) | 1981-11-19 |
| JPS5129165B2 (enrdf_load_stackoverflow) | 1976-08-24 |
| BR7209155D0 (pt) | 1973-09-25 |
| AU458574B2 (en) | 1975-02-03 |
| AU5042772A (en) | 1974-06-27 |
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